An experimental rectangular airlift reactor having mesh baffle-plates
has been fabricated out of Perspex and compared with conventional airl
ift and bubble column in terms of gas holdup, volumetric mass transfer
coefficient and mixing time. Mesh baffle-plates improved mass transfe
r and mixing with the mass transfer coefficient of the proposed reacto
r being up to 12% higher than that in a conventional airlift reactor u
nder the same operating condition. The mixing time of the proposed rea
ctor can be 95% lower than that of the airlift reactor.